US20050241531A1
2005-11-03
10/524,366
2003-07-29
US 7,563,317 B2
2009-07-21
WO; PCT/EP03/08329; 20030729
WO; WO2004/020531; 20040311
Patricia L Hailey
2023-07-29
Silanised, structurally modified silicas, characterised by groups fixed on the surface, the groups being alkylsilyl (SiCnH2n+1, with n=2-18). They are produced in that pyrogenically produced silicas are treated with the silanising agent and structurally modified. They are used to improve scratch resistance in lacquers.
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C04B14/04 IPC
Use of inorganic materials as fillers, e.g. pigments, for mortars, concrete or artificial stone; Treatment of inorganic materials specially adapted to enhance their filling properties in mortars, concrete or artificial stone; Granular materials, e.g. microballoons Silica-rich materials; Silicates
C01B33/12 IPC
Silicon; Compounds thereof; Silicon oxides; Hydrates thereof Silica; Hydrates thereof, e.g. lepidoic silicic acid
B82Y30/00 » CPC main
Nanotechnology for materials or surface science, e.g. nanocomposites
C09C1/3081 » CPC further
Treatment of specific inorganic materials other than fibrous fillers ; Preparation of carbon black; Compounds of silicon; Silicic acid Treatment with organo-silicon compounds
C09D7/62 » CPC further
Features of coating compositions, not provided for in group ; Processes for incorporating ingredients in coating compositions; Additives non-macromolecular inorganic modified by treatment with other compounds
C01P2004/64 » CPC further
Particle morphology; Particles characterised by their size Nanometer sized, i.e. from 1-100 nanometer
C01P2006/10 » CPC further
Physical properties of inorganic compounds Solid density
C01P2006/11 » CPC further
Physical properties of inorganic compounds Powder tap density
C01P2006/12 » CPC further
Physical properties of inorganic compounds Surface area
C01P2006/19 » CPC further
Physical properties of inorganic compounds Oil-absorption capacity, e.g. DBP values
C08K3/36 » CPC further
Use of inorganic substances as compounding ingredients; Silicon-containing compounds Silica
C08K9/06 » CPC further
Use of pretreated ingredients; Ingredients treated with organic substances with silicon-containing compounds
The invention relates to silanised, structurally modified, pyrogenically produced silicas, a process for the production thereof and their use.
Silanised silicas are used as thickeners, such as e.g. for water-thinnable lacquers and resins, such as e.g. epoxy resins.
From EP 0 672 731 B1, silanised, pyrogenically produced silicas are known, which are characterised in that the pyrogenically produced silicas are treated with a compound from the group (RO)3SiCnH2n+1, wherein n=10 to 18 and R=short-chained alkyl radicals. For example, the pyrogenically produced silicas have been treated with the compound (CH3O)3SiC16H33 (hexadecyltrimethoxysilane) or with the compound (CH3O)3SiC18H37 (octadecyltrimethoxysilane).
The production of the silanised, pyrogenically produced silicas takes place in that the pyrogenically produced silicas are placed in a mixer, the silicas are sprayed, optionally first with water and then with the compound from the group (RO)3SiCnH2n+1 while mixing intensively, mixed for a further 15 to 30 minutes and then tempered at a temperature of 100 to 160° C. for a period of 1 to 3 hours.
The invention provides silanised, structurally modified, pyrogenically produced silicas characterised by groups fixed on the surface, the groups being alkylsilyl (SiCnH2n+1, with n=2-18), preferably octylsilyl and/or hexadecylsilyl.
The silica according to the invention can have the following physico-chemical characteristics:
BET-surface area m2/g: 25-400
A silica produced by a high-temperature hydrolysis route from SiCl4+H2 and O2 can be used as the pyrogenically produced silica.
In particular, a silica produced by high temperature hydrolysis having the following physico-chemical characteristics can be used:
| TABLE 1 | ||||||||
| AEROSIL | AEROSIL | AEROSIL | AEROSIL | AEROSIL | AEROSIL | AEROSIL | AEROSIL | |
| 90 | 130 | 150 | 200 | 300 | 380 | OX 50 | TT 600 | |
| Behaviour in respect of water | hydrophilic |
| Appearance | loose white powder |
| BET surface area1) | m2/g | 90 ± 15 | 130 ± 25 | 150 ± 15 | 200 ± 25 | 300 ± 30 | 380 ± 30 | 50 ± 15 | 200 ± 50 |
| Average size of the | nm | 20 | 16 | 14 | 12 | 7 | 7 | 40 | 40 |
| primary particles | |||||||||
| Tamped density2) | |||||||||
| standard material | g/l | ca. 80 | ca. 50 | ca. 50 | ca. 50 | ca. 50 | ca. 50 | ca. 130 | ca. 60 |
| compacted material | g/l | — | ca. 120 | ca. 120 | ca. 120 | ca. 120 | ca. 120 | — | — |
| (additive “V”) | |||||||||
| Loss on drying3) | <1.0 | <1.5 | <0.59) | <1.5 | <1.5 | <1.5 | <1.5 | <2.5 | |
| (2 hours at 1000° C.) | % | ||||||||
| on leaving supplier's | |||||||||
| works | |||||||||
| Loss on ignition4)7) | % | <1 | <1 | <1 | <2 | <2 | <2.5 | <1 | <2.5 |
| (2 hours at 1000° C.) | |||||||||
| pH value5) (in 4% | 3.6-4.5 | 3.6-4.3 | 3.6-4.3 | 3.6-4.3 | 3.6-4.3 | 3.6-4.3 | 3.8-4.8 | 3.6-4.5 | |
| aqueous dispersion) | |||||||||
| SiO28) | % | >99.8 | >99.8 | >99.8 | >99.8 | >99.8 | >99.8 | >99.8 | >99.8 |
| Al2O38) | % | <0.05 | <0.05 | <0.05 | <0.05 | <0.05 | <0.05 | <0.08 | <0.05 |
| Fe2O38) | % | <0.003 | <0.003 | <0.003 | <0.003 | <0.003 | <0.003 | <0.01 | <0.003 |
| TiO28) | % | <0.03 | <0.03 | <0.03 | <0.03 | <0.03 | <0.03 | <0.03 | <0.03 |
| HCl8)9) | % | <0.025 | <0.025 | <0.025 | <0.025 | <0.025 | <0.025 | <0.025 | <0.025 |
| Sieving residue6) | % | <0.05 | <0.05 | <0.05 | <0.05 | <0.05 | <0.05 | <0.2 | <0.05 |
| (acc. to Mocker, | |||||||||
| 45 μm) | |||||||||
1)based on DIN 66131 |
|||||||||
2)based on DIN ISO 787/XI, JIS K 5101/18 (not sieved) |
|||||||||
3)based on DIN ISO 787/II, ASTM D 280, JIS K 5101/21 |
|||||||||
4)based on DIN 55 921, ASTM D 1208, JIS K 5101/23 |
|||||||||
5)based on DIN ISO 787/IX, ASTM D 1208, JIS K 5101/24 |
|||||||||
6)based on DIN ISO 787/XVIII, JIS K 5101/20 |
|||||||||
7)based on the substance dried for 2 hours at 105° C. |
|||||||||
8)based on the substance ignited for 2 hours at 1000° C. |
|||||||||
9)HCl content is a component of the loss on ignition |
Pyrogenic silicas of this type are known. They are described, inter alia, in:
The pyrogenically produced silicas are treated with a compound from the group (RO)3SiCnH2n+1, wherein n=2 to 18 and R=alkyl, such as e.g. methyl, ethyl or similar.
In particular, the following compounds can be used:
The silicas according to the invention can be produced in that the pyrogenically produced silicas are placed in a mixer, the silicas are sprayed, optionally first with water and then with the compound (organosilane) from the group (RO)3SiCnH2n+1 while mixing intensively, mixed for a further 15 to 30 minutes and then tempered at a temperature of 100 to 160° C. for a period of 1 to 3 hours, structurally modified and/or optionally post-ground. A further tempering can optionally take place after the structural modification and/or post-grinding.
The structural modification can take place e.g. with a ball mill or a continuously operating ball mill. The post-grinding can take place e.g. using an air-jet mill or pin mill. The tempering can take place batchwise, e.g. in a drying cupboard, or continuously, e.g. in a fluidised bed. The tempering can take place under protective gas, e.g. nitrogen.
The water used can be acidified with an acid, e.g. hydrochloric acid, down to a pH value of 7 to 1.
The organosilane used can be dissolved in a solvent, such as e.g. ethanol.
The tempering can be performed in a protective gas atmosphere, such as e.g. under nitrogen.
The pyrogenically produced silicas according to the invention silanised with silane I have the physico-chemical characteristics listed in Table 2 before structural modification:
| TABLE 2 | ||||||||
| Educt | A 90 | A 130 | A 150 | A 200 | A 300 | A 380 | OX 50 | TT 600 |
| Average size of the | 20 | 16 | 14 | 12 | 7 | 7 | 40 | 40 |
| primary particles | ||||||||
| [nm] | ||||||||
| BET surface area | 40-90 | 60-130 | 75-150 | 100-200 | 150-300 | 200-380 | 20-50 | 100-250 |
| [m2/g] | ||||||||
| Tamped density | 40-140 | 40-140 | 40-140 | 40-140 | 40-140 | 40-140 | 40-140 | 40-140 |
| [g/l] | ||||||||
| Loss on drying [%] | <2 | <2 | <2 | <2 | <2 | <2 | <2 | <2 |
| Loss on ignition | 0.1-10 | 0.1-10 | 0.1-10 | 0.5-15 | 0.5-20 | 0.5-25 | 0.1-10 | 0.1-20 |
| [%] | ||||||||
| C content [%] | 0.1-10 | 0.1-10 | 0.1-10 | 0.5-15 | 0.5-20 | 0.1-25 | 0.1-10 | 0.5-20 |
| pH value | 3.5-5.5 | 3.5-5.5 | 3.5-5.5 | 3.5-5.5 | 3.5-5.5 | 3.5-5.5 | 3.5-5.5 | 3.5-5.5 |
The silanised, structurally modified, pyrogenically produced silicas according to the invention can be used to improve scratch resistance in lacquers.
EXAMPLESThe pyrogenically produced silicas used have the physico-chemical characteristics listed in Table 1.
As organosilanes, the following compound with the general formula (RO)3SiCnH2n+1 is used:
The silica is placed in a mixer and sprayed first with water and then with organosilane, mixing intensively.
When the spraying is complete, stirring is continued for a further 15 to 30 minutes and then the mixture is tempered for 1 to 3 hours at 100 to 160° C. The tempering can also take place under protective gas, e.g. nitrogen.
The individual reaction conditions can be taken from Table 3.
The physico-chemical characteristics of the silanised silicas obtained are listed in Table 4.
| TABLE 3 | |||||||
| Tem- | |||||||
| Silane | Water | Ethanol | Tem- | pering | |||
| Ex- | quantity | quantity | quantity | pering | temper- | ||
| am- | (g/100 g | (g/100 g | (g/100 g | period | ature | ||
| ple | Aerosil | Silane | Aerosil) | Aerosil) | Aerosil) | (h) | (° C.) |
| 1 | A 300 | Silane I | 1 | 0 | 9 | 2 | 120 |
| 2 | A 200 | Silane I | 2.5 | 0 | 0 | 2 | 140 |
| 3 | A 200 | Silane I | 20 | 5 | 0 | 2 | 140 |
| 4 | A 200 | Silane I | 10 | 2.5 | 0 | 2 | 140 |
| 5 | A 200 | Silane I | 5 | 1.25 | 0 | 2 | 140 |
| 6 | A 200 | Silane I | 2.5 | 1.25 | 0 | 2 | 140 |
| TABLE 4 | ||||||
| Tamped | Surface | Loss on | Loss on | |||
| density | C content | area | drying | ignition | ||
| Example | pH value | (g/l) | (%) | (m2/g) | (%) | (%) |
| 1 | 4.3 | 50 | 1.3 | 253 | 0.4 | 1.8 |
| 2 | 4.4 | 49 | 1.7 | 176 | 0.3 | 2.5 |
| 3 | 4.6 | 68 | 10.1 | 116 | 0.6 | 12.7 |
| 4 | 4.5 | 72 | 5.7 | 144 | 0.6 | 7.1 |
| 5 | 4.7 | 52 | 2.6 | 167 | 0.6 | 3.4 |
| 6 | 4.5 | 51 | 1.9 | 171 | 0.7 | 2.5 |
The silicas, which can be produced as described in EP 0 672 731, are then structurally modified by mechanical action and possibly post-ground in a mill. A tempering can possibly take place after the structural modification and/or post-grinding.
The structural modification can take place e.g. with a ball mill or a continuously operating ball mill. The post-grinding can take place e.g. using an air-jet mill or pin mill. The tempering can take place batchwise, e.g. in a drying cupboard, or continuously, e.g. in a fluidised bed. The tempering can take place under protective gas, e.g. nitrogen.
| TABLE 5 |
| Overview of the production of the comparative silicas and |
| the silicas according to the invention (Examples) |
| Post- | ||||
| grinding | ||||
| after | Tempering | |||
| Surface-fixed | Structural | structural | after | |
| Designation | group | modification | modification | post-grinding |
| Comparative | Hexadecylsilyl | No | — | — |
| silica 1 | ||||
| Comparative | Octylsilyl | No | — | — |
| silica 2 | ||||
| Silicas 1 | Hexadecylsilyl | Yes | No | No |
| Silicas 2 | Octylsilyl | Yes | Yes | No |
| Silicas 3 | Hexadecylsilyl | Yes | Yes | Yes |
| Silicas 4 | Octylsilyl | Yes | No | Yes |
| Silicas 5 | Octylsilyl | Yes | Yes | No |
| Silicas 6 | Hexadecylsilyl | Yes | Yes | No |
| Silicas 7 | Hexadecylsilyl | Yes | Yes | No |
| Silicas 8 | Hexadecylsilyl | Yes | No | No |
| Silicas 9 | Octylsilyl | Yes | Yes | No |
| Silicas 10 | Octylsilyl | Yes | No | No |
| Silicas 11 | Octylsilyl | Yes | Yes | No |
| Silicas 12 | Octylsilyl | Yes | No | No |
| TABLE 6 |
| Physico-chemical data of the silicas according to the invention (Examples) |
| and the comparative silicas |
| Tamped | Loss on | DBP | BET specific | ||||
| density | Loss on | ignition | adsorption | surface area | |||
| Designation | [g/l] | drying [%] | [%] | pH value | C content [%] | [%] | [m2/g] |
| Comparative silica 1 | 57 | 0.5 | 1.8 | 4.6 | 1.2 | 302 | 195 |
| Comparative silica 2 | 51 | 0.6 | 6.8 | 5.3 | 5.4 | 263 | 175 |
| Silicas 1 | 137 | 0.7 | 1.9 | 4.9 | 1.3 | 217 | 193 |
| Silicas 2 | 112 | 0.7 | 7.0 | 5.8 | 5.5 | 145 | 175 |
| Silicas 3 | 118 | 0.7 | 2.3 | 5.1 | 1.3 | 228 | 176 |
| Silicas 4 | 163 | 0.9 | 6.7 | 5.3 | 5.4 | 134 | 176 |
| Silicas 5 | 114 | 0.5 | 7.1 | 6.0 | 5.4 | 142 | 175 |
| Silicas 6 | 113 | 1.3 | 2.2 | 5.1 | 1.4 | 221 | 193 |
| Silicas 7 | 123 | 0.7 | 2.6 | 6.0 | 1.4 | 208 | 197 |
| Silicas 9 | 146 | 1.1 | 2.3 | 5.8 | 1.4 | 182 | 195 |
| Silicas 9 | 240 | 0.8 | 6.7 | 4.8 | 5.3 | 87 | 169 |
| Silicas 10 | 322 | 0.3 | 6.9 | 6.0 | 5.3 | Could not | 172 |
| be | |||||||
| determined | |||||||
| Silicas 11 | 204 | 0.7 | 6.4 | 5.7 | 5.4 | 101 | 173 |
| Silicas 12 | 276 | 0.3 | 6.6 | 6.6 | 5.3 | Could not | 168 |
| be | |||||||
| determined | |||||||
For the investigation of the improvement in scratch resistance, a conventional 2-component polyurethane lacquer was used. The formulation of the lacquer and its production, including application, are summarised below:
Formulation:
| Parts | |
| by wt. | |
| Millbase | ||
| Acrylic resin, 50% in xylene/ethylbenzene 3:1 | 53.3 | |
| Butyl acetate 98% | 6.7 | |
| Xylene | 6.7 | |
| Silica | 5.0 | |
| Σ | 71.7 | |
| Lacquer make-up | ||
| Acrylic resin, 50% in xylene/ethylbenzene 3:1 | 1.1 | |
| Xylene | 12.2 | |
| Ethoxypropyl acetate | 1.5 | |
| Butyl glycol acetate | 1.5 | |
| Butyl acetate 98% | — | |
| Aliphatic polyisocyanate, approx. 75% in 1- | 17.0 | |
| methoxypropyl-2-acetate/xylene 1:1 | ||
| Σ | 105.0 | |
The binder is mixed with the solvents. Then, for the purpose of predispersion, the silica is incorporated into this mixture with the high-speed mixer (disk Ø 45 mm) and predispersed for 5 min at 2000 rpm. The mixture is dispersed in a laboratory pearl mill for 30 min at 2500 rpm and 60% pump capacity using glass beads (Ø approx. 1 mm). The millbase is tested with a grindometer, 25 μm, according to DIN ISO 1524. It must be smaller than 10 μm.
The conversion of the millbase to lacquer takes place in accordance with the formulation, the components being mixed at 2000 rpm with a vane agitator. The hardener is incorporated in the same way.
After adjusting the lacquers to spray viscosity in accordance with DIN 53411, the lacquers are applied to black lacquered metal sheets, e.g. DT 36 (from Q-Panel), by spray application (coat thickness about 40-50 μm). After spraying, the metal sheets are dried for 24 h at room temperature and then for 2 h in a drying oven at 70° C.
Scratch Tests:
The metal sheets are abraded with a quartz/water slurry (100 g water+1 g Marlon A 350, 0.25%+5 g Sikron F500) and with a CaCO3/water mixture (100 g water+1 g Marlon A 350, 0.25%+5 g Millicarb BG) using an abrasion and washing resistance tester (Erichsen, brush with hog's bristles). The gloss before and 10 min after the abrading is determined with a reflectometer (200 irradiation angle).
| TABLE 7 |
| Summary of the properties of the liquid lacquers relevant in terms of lacquer technology, |
| and of the applied and dried films. |
| Reference | Reference | |||||||
| Comparative | without | Comparative | Silica | without | ||||
| silica 1 | Silica 7 | Silica 8 | silica | silica 2 | Silica 9 | 11 | silica | |
| Grindometer value [μm] | <10 | <10 | <10 | <10 | <10 | <10 | <10 | / |
| Viscosity (millbase) [mPas] | ||||||||
| 6 Rpm | 409 | 210 | 220 | / | 5670 | 935 | 832 | / |
| 60 Rpm | 407 | 210 | 212 | / | 1260 | 409 | 407 | / |
| Viscosity (lacquer + hardener) | ||||||||
| [mPas] | ||||||||
| 6 rpm | 120 | 80 | 80 | 60 | 446 | 195 | 175 | 55 |
| 60 rpm | 113 | 82 | 82 | 61 | 194 | 146 | 144 | 64 |
| Flow | poor | OK | OK | OK | Orange peel | OK | OK | OK |
| fine cracks | effect |
| Scratch resistance |
| 20° reflectometer value | 81 | 89.5 | 89.1 | 91.3 | 38 | 85.5 | 85.3 | 91.7 |
| before scratching | ||||||||
| Haze before scratching | 101 | 9 | 12 | 2 | 423 | 18 | 19 | 2 |
| Black value My | 272 | 286 | 286 | 291 | 260 | 283 | 282 | 294 |
| 40 strokes with Sikron | 83.4 | 88.5 | 90.7 | 51.8 | / | 80.4 | 84.3 | 56.1 |
| F 500 residual gloss [%] | ||||||||
The silicas 7+8 and 9+11 according to the invention can be used in high concentrations without impairing the appearance of the lacquer surface owing to their substantially lower rheological efficiency compared with comparative silica 1+2. In addition, the silicas according to the invention display a substantial improvement in scratch resistance of the lacquer surface.
Example 2In this example the influence of the structural modification was investigated on the basis of a high solids 2-component PU clear lacquer. The formulation of the lacquer and its production, including application and testing, are summarised below:
Formulation:
| Parts by | |
| wt. | |
| Millbase | ||
| Acrylic copolymer, mod. with synthetic | 61.0 | |
| fatty acids, 70% in n-butyl acetate | ||
| Butyl acetate 98% | 7.3 | |
| Methoxypropyl acetate | 1.7 | |
| Solvesso 100 | 2.0 | |
| Xylene | 2.0 | |
| Baysilon OL 17, 10% in xylene (silicone | 0.7 | |
| oil) | ||
| Silica | 5.0 | |
| Σ | 79.7 | |
| Lacquer make-up (hardener) | ||
| Aliphatic polyisocyanate, 90% in n- | 22.3 | |
| butyl acetate | ||
| Butyl acetate 98% | 2.0 | |
| Solvesso 100 | 1.0 | |
| Σ | 105.0 | |
The binder is mixed with the solvents. Then, for the purpose of predispersion, the silica is incorporated into this mixture with the high-speed mixer (disk Ø 45 mm) and predispersed for 5 min at 2000 rpm. The mixture is dispersed in a laboratory pearl mill for 30 min at 2500 rpm and 60% pump capacity using glass beads (Ø approx. 1 mm). The millbase is tested with a grindometer, 25 μm, in accordance with DIN ISO 1524. It must be smaller than 10 μm.
The conversion of the millbase to lacquer takes place in accordance with the formulation, the components being mixed with a vane agitator at 2000 rpm. The hardener is incorporated in the same way.
After adjusting the lacquers to spray viscosity in accordance with DIN 53411, the lacquers are applied to black lacquered metal sheets, e.g. DT 36 (from Q-Panel), by spray application (coat thickness about 40-50 μm). After spraying, the metal sheets are dried for 24 h at room temperature and then for 2 h in a drying oven at 70° C.
Scratch Tests:
The metal sheets are abraded with a quartz/water slurry (100 g water+1 g Marlon A 350, 0.25%+5 g Sikron F500) using an abrasion and washing resistance tester (Erichsen, brush with hog's bristles). The gloss before and 10 min after the abrading is determined with a reflectometer (20° irradiation angle).
| TABLE 8 |
| Summary of the properties of the liquid lacquers |
| relevant in terms of lacquer technology, and of the applied |
| and dried films. |
| Reference | ||||
| Comparative | Silica | without | ||
| silica 1 | silica 7 | 8 | Silica | |
| Bulk density [g/l] | 50 | 146 | 123 | / |
| Grindometer value [μm] | <10 | <10 | <10 | / |
| Viscosity (millbase) | ||||
| [mPas] | ||||
| 6 rpm | 767 | 376 | 376 | 205 |
| 60 rpm | 717 | 359 | 361 | 205 |
| Viscosity (lacquer + hardener) | ||||
| [mPas] | ||||
| 6 rpm | 459 | 279 | 281 | 120 |
| 60 rpm | 399 | 272 | 274 | 120 |
| Flow | poor (fine | OK | OK | OK |
| “cracks”) |
| Scratch resistance |
| 20° reflectometer | 82.3 | 86.5 | 86.3 | 88.2 |
| value before | ||||
| scratching | ||||
| Haze before scratching | 3 | 4 | 4 | 2 |
| Black value My | 275 | 283 | 282 | 292 |
| 40 strokes with | 63.2 | 78.2 | 75.4 | 30.2 |
| Sikron F 500 | ||||
| residual gloss [%] | ||||
The silicas 7+8 according to the invention can be used in high concentrations without impairing the appearance of the lacquer surface owing to their substantially lower Theological efficiency compared with comparative silica 1. In addition, the silicas according to the invention display a substantial improvement in the scratch resistance of the lacquer surface.
Example 3For the investigation of the improvement of the scratch resistance, a conventional 2-component polyurethane lacquer was used. The formulation of the lacquer and its production, including its application, are summarised below:
Formulation
| Parts by wt. | ||
| Millbase | ||
| Acrylic copolymer, mod. with | 43.4 | |
| synthetic fatty acids, 60% solution | ||
| Butyl acetate 98% | 17.8 | |
| Xylene | 3.9 | |
| Silica | 5.0 | |
| Σ | 70.7 | |
| Lacquer make-up | ||
| Xylene | 11.3 | |
| Ethoxypropyl acetate | 3.4 | |
| Butyl glycol acetate | 1.6 | |
| Aliphatic polyisocyanate, approx. | 18.6 | |
| 75% in 1-methoxypropyl-2- | ||
| acetate/xylene 1:1 | ||
| Σ | 105.0 | |
The binder is mixed with the solvents. Then, for the purpose of predispersion, the silica is incorporated into this mixture with the high-speed mixer (disk Ø 45 mm) and predispersed for 5 min at 2000 rpm. The mixture is dispersed in a laboratory pearl mill for 30 min at 2500 rpm and 60% pump capacity using glass beads (Ø approx. 1 mm). The millbase is tested with a grindometer, 25 μm, in accordance with DIN ISO 1524. It must be smaller than 10 μm.
The conversion of the millbase to lacquer takes place in accordance with the formulation, the components being mixed with a vane agitator at 2000 rpm. The hardener is incorporated in the same way.
After adjusting the lacquers to spray viscosity in accordance with DIN 53411, the lacquers are applied to black lacquered metal sheets, e.g. DT 36 (from Q-Panel), by spray application (coat thickness about 40-50 μm). After spraying, the metal sheets are dried for 24 h at room temperature and then for 2 h in a drying oven at 70° C.
Scratch Tests:
The metal sheets are abraded with a quartz/water slurry (100 g water+1 g Marlon A 350, 0.25%+5 g Sikron F500) using an abrasion and washing resistance tester (Erichsen, brush with hog's bristles). The gloss before and 10 min after the abrading is determined with a reflectometer (20° irradiation angle).
| TABLE 9 |
| Summary of the properties of the liquid lacquers relevant in terms of lacquer technology, |
| and of the applied and dried films. |
| Reference | Reference | |||||||
| Comparative | without | Comparative | Silica | without | ||||
| silica 1 | Silica 7 | Silica 8 | silica | silica 2 | Silica 9 | 11 | silica | |
| Grindometer value [μm] | <10 | <10 | <10 | / | <10 | <10 | <10 | / |
| Viscosity (millbase) | ||||||||
| [mPas] | ||||||||
| 6 rpm | 409 | 210 | 220 | / | 5670 | 935 | 832 | / |
| 60 rpm | 407 | 210 | 212 | / | 1260 | 409 | 407 | / |
| Viscosity (lacquer + hardener) | ||||||||
| [mPas] | ||||||||
| 6 rpm | 120 | 80 | 80 | 60 | 446 | 195 | 175 | 55 |
| 60 rpm | 113 | 82 | 82 | 61 | 194 | 146 | 144 | 64 |
| Flow | Poor | OK | OK | OK | Orange-peel | OK | OK | OK |
| fine cracks | effect |
| Scratch resistance |
| 20° reflectometer | 81 | 89.5 | 89.1 | 91.3 | 38 | 85.5 | 85.3 | 91.7 |
| value before | ||||||||
| scratching | ||||||||
| Haze before scratching | 101 | 9 | 12 | 2 | 423 | 18 | 19 | 2 |
| 40 strokes with Sikron | 83.4 | 88.5 | 90.7 | 51.8 | / | 80.4 | 84.3 | 56.1 |
| F 500 | ||||||||
| Residual gloss [%] | ||||||||
The silicas 7+8 and 9+10 according to the invention can be used in high concentrations without impairing the appearance of the lacquer surface owing to their substantially lower rheological efficiency compared with comparative silica 1 and 2. In addition, the silicas according to the invention display a substantial improvement in the scratch resistance of the lacquer surface.
Example 4Direct comparison of the silicas according to the invention with a scratch-resistant lacquer according to DE 198 11 790 A1, in which AEROSIL R 972 is used to improve the scratch resistance.
| Silicas 2) | ||
| Prior art | according to the | |
| 1) | invention | |
| Millbase | |||
| Desmophen A 2009/1 | 190.2 | ||
| Methoxypropyl acetate:Solvesso | 36.8 | ||
| 100 1:1 | |||
| Silica | 23.0 | ||
| Σ | 250.0 | ||
| Lacquer make-up | |||
| Desmophen A YEP4-55A, | 96.0 | — | |
| contains AEROSIL R 972 | |||
| Millbase | — | 48.9 | |
| Desmophen 2009/1 | — | 24.9 | |
| OL 17, 10% in MPA | — | — | |
| Modaflow 1% in MPA | — | — | |
| MPA:Solvesso 100 | 11.6 | 33.8 | |
| 1:1 | |||
| Butyl glycol acetate | 10.5 | 10.5 | |
| Byketol OK | 7.5 | 7.5 | |
| Byk 141 | 0.8 | 0.8 | |
| Addition of hardener | |||
| Desmodur N 3390 | 23.6 | 23.6 | |
| Σ | 150.0 | 150.0 | |
The conversion to lacquer of the millbases corresponding to 1) or 2) takes place in accordance with the formulation, the components being mixed at 2000 rpm with a vane agitator. The hardener is incorporated in the same way.
After adjusting the lacquers to spray viscosity in accordance with DIN 53411, the lacquers are applied to black lacquered metal sheets, e.g. DT 36 (from Q-Panel), by spray application (coat thickness about 40-50 μm). After spraying, the metal sheets are dried for 24 h at room temperature and then for 2 h in a drying oven at 70° C.
Scratch Tests:
The metal sheets are abraded with a CaCO3/water slurry (100 g water+1 g Marlon A 350, 0.25%+5 g Millicarb CaCO3) using an abrasion and washing resistance tester (Erichsen, brush with hog's bristles). The gloss before and 10 min after the abrading is determined with a reflectometer (20° irradiation angle).
| TABLE 10 |
| Summary of the properties of the liquid lacquers |
| relevant in terms of lacquer technology, and of the applied |
| and dried films. |
| Prior art | Silica 7 | Reference | ||
| Grindometer value | <10 | <10 | / | |
| [μm] | ||||
| Viscosity (millbase) | ||||
| [mPas] | ||||
| 6 rpm | 58 | 30 | 30 | |
| 60 rpm | 48 | 43 | 40 | |
| Surface | Orange | OK | OK | |
| peel | ||||
| 20° reflectometer | 88.0 | 86.5 | 98.5 | |
| value before | ||||
| scratching | ||||
| 100 strokes with | 88.6 | 96.3 | 59.6 | |
| Millicarb | ||||
| Residual gloss [%] | ||||
It is shown that a substantially better improvement in the residual gloss is achieved after a scratch stressing of the lacquer surface by using the silica according to the invention than with the prior art. In addition, owing to its low rheological efficiency, the silica according to the invention does not cause an orange-peel effect.
1. Silanised, structurally modified, pyrogenically produced silicas,
characterised by groups fixed to the surface, wherein the groups are alkylsilyl (SiCnH2n+1, with n=2-18).
2. Silanised, structurally modified, pyrogenically produced silicas according to claim 1,
characterised in that the pyrogenically produced silicas have been treated with the compound (CH3O)3SiC16H33 (hexadecyltrimethoxysilane).
3. Silanised, structurally modified, pyrogenically produced silicas according to claim 1,
characterised in that the pyrogenically produced silicas have been treated with the compound (CH3O)3SiC8H17 (octyltrimethoxysilane).
4. Process for the production of the silanised, structurally modified, pyrogenically produced silicas according to claim 1,
characterised in that the pyrogenically produced silicas are placed in a mixer, the silicas are sprayed, optionally first with water and then with the compound from the group (RO)3SiCnH2n+1 while mixing intensively, mixed for a further 15 to 30 minutes and then tempered at a temperature of 100 to 160° C. for a period of 1 to 3 hours, structurally modified and/or optionally post-ground.
5. Process for the production of the silanised, structurally modified, pyrogenically produced silicas according to claim 4,
characterised in that an additional tempering is allowed to follow the structural modification and/or post-grinding.
6. Use of the silanised, structurally modified, pyrogenically produced silicas to improve the scratch resistance of lacquers.
7. A silanised, structurally modified, pyrogenically produced silica, having alkylsilyl groups of the formula SiCnH2n+1, with n=2-18.
8. The silanised structurally modified, pyrogenically produced silica according to claim 7, having the following physical chemical properties:
BET surface area 25-400 m2/g
Average size of primary particles 5-50 nm
pH value 3-10
Carbon content 0.1-25%
DBP value in % at least 10% lower than the DBP value of a corresponding silianised, non-structurally modified silica
9. The silanised, structurally modified, pyrogenically produced silica according to claim 7, wherein the pyrogenically produced silica has been treated with the compound (CH3O)3SiC16H33.
10. The silanised, structurally modified, pyrogenically produced silica according to claim 7, wherein the pyrogenically produced silica has been treated with the compound (CH3O)3SiC8H17.
11. A process for the production of the silanised, structurally modified, pyrogenically produced silica according to claim 7, comprising placing the pyrogenically produced silica in a mixer, spraying the silica, optionally first with water, and then spraying with a compound having the formula (RO)3SiCnH2n+1 wherein n is 2 to 18 and R is alkyl, while mixing intensively, mixing for a further 15 to 30 minutes and then tempering at a temperature of 100 to 160° C. for a period of 1 to 3 hours, structurally modifying and/or optionally post-grinding.
12. The process for the production of the silanised, structurally modified, pyrogenically produced silica according to claim 11, further comprising additionally tempering following structural modification and/or post-grinding.
13. The process according to claim 11, wherein structurally modifying takes place by ball milling.
14. The process according to claim 11, wherein post grinding takes place by using an air-jet mill or pin mill.
15. The process according to claim 12, wherein tempering takes place in a drying cupboard or in a fluidized bed.
16. The process according to claim 15, wherein the tempering takes place under protective gas.
17. A lacquer containing the silanised, structurally modified, pyrogenically produced silica of claim 1.
18. A lacquer containing the silanised, structurally modified, pyrogenically produced silica of claim 7.
19. A surface having applied thereto a coating produced from the lacquer of claim 17.
20. The surface according to claim 19, which is metal.